WO2006117977A1 - Process for production of carbostyril compound - Google Patents

Process for production of carbostyril compound Download PDF

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Publication number
WO2006117977A1
WO2006117977A1 PCT/JP2006/307461 JP2006307461W WO2006117977A1 WO 2006117977 A1 WO2006117977 A1 WO 2006117977A1 JP 2006307461 W JP2006307461 W JP 2006307461W WO 2006117977 A1 WO2006117977 A1 WO 2006117977A1
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Prior art keywords
compound
formula
salt
reaction
acid
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PCT/JP2006/307461
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French (fr)
Japanese (ja)
Inventor
Kengo Kawasaki
Takayuki Ikeda
Kenji Sekine
Norio Fukuda
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Otsuka Pharmaceutical Co., Ltd.
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Application filed by Otsuka Pharmaceutical Co., Ltd. filed Critical Otsuka Pharmaceutical Co., Ltd.
Priority to US11/596,004 priority Critical patent/US7718806B2/en
Priority to CN2006800004646A priority patent/CN1989108B/en
Publication of WO2006117977A1 publication Critical patent/WO2006117977A1/en
Priority to IL179235A priority patent/IL179235A/en
Priority to KR1020067024388A priority patent/KR101265877B1/en

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D215/00Heterocyclic compounds containing quinoline or hydrogenated quinoline ring systems
    • C07D215/02Heterocyclic compounds containing quinoline or hydrogenated quinoline ring systems having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen atoms or carbon atoms directly attached to the ring nitrogen atom
    • C07D215/16Heterocyclic compounds containing quinoline or hydrogenated quinoline ring systems having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen atoms or carbon atoms directly attached to the ring nitrogen atom with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
    • C07D215/20Oxygen atoms
    • C07D215/22Oxygen atoms attached in position 2 or 4
    • C07D215/227Oxygen atoms attached in position 2 or 4 only one oxygen atom which is attached in position 2
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D215/00Heterocyclic compounds containing quinoline or hydrogenated quinoline ring systems
    • C07D215/02Heterocyclic compounds containing quinoline or hydrogenated quinoline ring systems having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen atoms or carbon atoms directly attached to the ring nitrogen atom
    • C07D215/16Heterocyclic compounds containing quinoline or hydrogenated quinoline ring systems having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen atoms or carbon atoms directly attached to the ring nitrogen atom with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
    • C07D215/20Oxygen atoms
    • C07D215/22Oxygen atoms attached in position 2 or 4
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00Medicinal preparations containing organic active ingredients
    • A61K31/33Heterocyclic compounds
    • A61K31/395Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins
    • A61K31/435Heterocyclic compounds having nitrogen as a ring hetero atom, e.g. guanethidine or rifamycins having six-membered rings with one nitrogen as the only ring hetero atom
    • A61K31/47Quinolines; Isoquinolines
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P1/00Drugs for disorders of the alimentary tract or the digestive system
    • A61P1/04Drugs for disorders of the alimentary tract or the digestive system for ulcers, gastritis or reflux esophagitis, e.g. antacids, inhibitors of acid secretion, mucosal protectants
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides

Definitions

  • the present invention relates to an improved method for producing a carbostyril compound, which produces the following carbostyril compound which is useful as a therapeutic agent for gastric ulcer and the like more safely and efficiently.
  • the carboschirirui compound of the present invention is a carboschirirui compound represented by the following formula (1) (chemical name: 2— (4 black benzoylamino)-3- [2 (1 ⁇ ) -quinolinone 4-yl] propionic acid), a drug that exhibits excellent therapeutic effects on gastric mucosal lesions appearing during gastric ulcer, acute gastritis, or acute exacerbation of chronic gastritis.
  • formula (1) chemical name: 2— (4 black benzoylamino)-3- [2 (1 ⁇ ) -quinolinone 4-yl] propionic acid
  • Patent Document 1 a method represented by the following reaction formula 1 is known (Patent Document 1). That is, the compound of formula (2) is reacted with the compound of formula (3) in the presence of a base such as sodium ethoxide to obtain the compound of formula (4), and this compound is hydrolyzed with a mineral acid such as hydrochloric acid. And decarboxylating to produce the compound of formula (5), and then saponifying with 4-chlorobenzoyl chloride of formula (6) to produce the desired compound of formula (1).
  • a base such as sodium ethoxide
  • a mineral acid such as hydrochloric acid
  • the step of producing the compound of the formula (5) from the compound of the formula (4) is required to heat and reflux the compound (4) in, for example, 20% hydrochloric acid.
  • the reaction interface is bubbling violently due to the generated carbon dioxide gas, and this foam does not disappear immediately.
  • the amount of hydrochloric acid relative to compound (4) is small, a rapid increase in the interface due to the bubbles is observed, and it is often difficult to carry out the refluxing continuously.
  • Patent Document 1 Japanese Patent Application Laid-Open No. 60-19767
  • An object of the present invention is to provide an improved method by which a carbostyril compound of formula (1) or a salt thereof useful as a medicament can be produced more safely and efficiently.
  • the compound of formula (5) or a salt thereof produced as an intermediate in the production method of the present invention is an intermediate substance for producing a desired carbostyril compound or a salt thereof of formula (1). It is desired that the crystal can be easily and easily removed from the reaction system. Moreover, in order to be suitable for storage as an intermediate substance for producing a desired carboschiril compound of the formula (1) or a salt thereof, it is desired that the drying can be performed more easily and efficiently. .
  • Another object of the present invention is to provide a compound of the formula (4) during a series of steps for producing the desired carbostyril compound of the formula (1) or a salt thereof from the compound of the formula (2) or a salt thereof.
  • heating in the presence of a high-boiling point solvent suitable for this step causes a sudden reaction caused by bubbles generated during the reaction.
  • the present invention provides a method for more safely producing the desired carbostyryl compound (formula (1)) or a salt thereof by suppressing the rise of the interface and bumping accompanying this.
  • Another object of the present invention is to improve the above-mentioned problem of preventing bumping, while maintaining the reflux temperature while removing by-products such as ethanol and ethyl acetate in the reaction step as necessary.
  • the present invention also provides a method for producing the compound 5) or a salt thereof more efficiently.
  • a further object of the present invention is to provide a dihydrochloride dihydrate of the compound of formula (5) as the desired intermediate.
  • the compound of formula (5) or a salt thereof can be produced safely by heating the compound of formula (4) or a salt thereof in the presence of a high-boiling solvent under acidic conditions.
  • the production of the compound of formula (5) or a salt thereof can be carried out more efficiently by maintaining the heating temperature, particularly the reflux temperature, while removing by-products such as ethanol and ethyl acetate in the reaction step as necessary. Can do.
  • the compound (5) or a salt thereof is acylated with 4 chlorobenzoyl chloride of the formula (6) to obtain the target carbostyryl compound of the formula (1) or a salt thereof.
  • the reaction when the compound of the formula (4) or a salt thereof is heated under acidic conditions to derive the compound of the formula (5) or a salt thereof, the reaction is performed with a specific high boiling point solvent.
  • the high boiling point solvent functions as an antifoaming agent, suppresses undesirable foaming, and adds sufficient caloric heat to accelerate the reaction.
  • the step of heating the compound of the formula (4) or a salt thereof to obtain the compound of the formula (5) or a salt thereof is performed in water, and Z or of the formula (5) Reaction process power to obtain a target carbostyril compound of the formula (1) or a salt thereof by subjecting the compound or a salt thereof to acylation
  • the above formula (5) carried out in water, an organic solvent or a mixture thereof Or a salt thereof, or a method for producing a carbostyril compound of the formula (1) or a salt thereof.
  • a reaction in which the heating reaction is carried out in the presence of hydrochloric acid ( 5) A method for producing a compound or a salt thereof can be provided.
  • the high boiling point solvent used in the step of heating the compound of the formula (4) or a salt thereof to obtain the compound of the formula (5) or a salt thereof is normal octanol and Z
  • the compound of the formula (5) or a salt thereof obtained by the production method of the present invention is a dihydrochloride dihydrate of the compound represented by the formula (5). It is possible to provide new substances with features.
  • the high boiling point solvent used in the present invention may be any substance that can perform the above-described operation without any trouble.
  • the solvent is a substance that can suppress the rise of the interface due to foaming caused by the generation of the carbon dioxide gas, and It must azeotrope with the solvent added with the acid used in the reaction, have a higher specific gravity than the solvent added with the acid, and be separated without mixing with the solvent added with the acid, and have a higher boiling point than the solvent added with the acid. Has been found to be suitable for that purpose.
  • the inventors of the present invention can preferably illustrate hydrochloric acid as the acid used in the production method of the present invention, as shown in the examples below, and the corresponding high-boiling solvent has a specific gravity higher than that of hydrochloric acid, for example. It has been found that normal otatanol and Z or acetophenone, which are high-boiling substances that are not mixed with small hydrochloric acid, are more suitable for that purpose.
  • the reaction leading to the compound of formula (4) or a salt thereof by acid hydrolysis to the compound of formula (5) or a salt thereof is carried out by using a high-boiling solvent in the presence of a hydrolysis catalyst. It is done by adding.
  • Hydrolysis catalysts include halogen hydrofluoric acids such as hydrochloric acid, hydrobromic acid and hydroiodic acid, mineral acids such as sulfuric acid and phosphoric acid, and organic acids such as formic acid, acetic acid, trifluoroacetic acid and p-toluenesulfonic acid.
  • hydrochloric acid can be exemplified.
  • catalysts can be used singly or in combination of two or more.
  • water contained in hydrochloric acid which may be used as the reaction solvent with a solvent such as water in which the acid is dissolved, is particularly preferred as the solvent for the reaction.
  • the amount of acid used as the catalyst is not particularly limited.
  • hydrochloric acid is used as the acid.
  • it can also be used as a solvent for the reaction, and the concentration is usually
  • the high boiling point solvent that can be used in the present invention results from the generation of carbon dioxide gas by-produced in the step of heating and reacting the compound of the above formula (4) or a salt thereof under acidic conditions. It exists as a substance (including defoaming effect) that can suppress the rise of the interface due to foaming (including defoaming), does not mix with the solvent to which the acid is added, and is used for the reaction. There is no particular limitation as long as it is a substance that has physico-chemical properties that azeotropes with the solvent to which the acid is added and has a higher boiling point and lower specific gravity than the solvent to which the acid is added. .
  • high boiling point solvent examples include normal pentanol, 2-pentanol, 3-pentanol, 3-methyl-1-butanol, normal hexanol, 2-methyl-1-pentanol, 2-ethyl-1-butanol, and 3 Ptanol, normal otathanol, normal nonanol, 3, 5, 5 trimethyl- 1 hexanol, normalde force norm, normalunde force norl, normal dodecanol etc.
  • hydrochloric acid is used also as an acid catalyst and a solvent for the reaction
  • normaloctanol and acetophenone having physical and physical properties satisfying the above conditions are more suitable. It can be used as a high boiling point solvent.
  • the amount of the high-boiling solvent used is not particularly limited, and the preferred amount varies depending on the degree of foaming, the shape of the reaction vessel, etc., but with respect to 1 part by weight of the compound of formula (4) or a salt thereof, Usually, a range force of about 0.1 to 3 parts by volume, preferably about 0.1 to 1 parts by volume is also selected.
  • the above reaction is usually carried out by heating from 80 ° C. to the reflux temperature of the reaction solvent, preferably 100 ° C. and the reaction solvent, and is usually completed in about 6 to 24 hours.
  • the high-boiling solvent used in the production method of the present invention has the effect of suppressing an increase in the reaction liquid interface in the step of heating and reacting the compound of formula (4) or a salt thereof under acidic conditions. Since the compound of formula (5) or a salt thereof can be produced safely and the volumetric efficiency of the reactor can be greatly increased, it can be used for mass synthesis of the compound of formula (5) or a salt thereof. It can be suitably used.
  • the compound of the formula (5) In the reaction leading to the compound or its salt, the compound of the formula (5) or its salt is more efficiently produced by maintaining the heating temperature, particularly the reflux temperature while removing by-products in the reaction step as necessary. be able to.
  • the above two conditions can be satisfied at the same time, which can be suitably used as an industrial production method.
  • the azeotropic water and high-boiling point solvent condensate are separated into two layers in the apparatus, and the high-boiling point solvent used in the production method of the present invention is separated into the upper layer.
  • the resulting low-boiling substances are distributed to the lower layer (aqueous layer; eg hydrochloric acid). Therefore, by extracting only the lower layer little by little, low-boiling substances are removed from the reaction system, the necessary high reflux temperature is maintained and reaction delay is avoided, and only the upper-boiling solvent in the upper layer is circulated to the reaction tank. And the rise of the interface due to foaming can be continuously suppressed.
  • the high-boiling solvent and water (including acid) are removed by extracting the condensate out of the reaction system and separating it without circulating the high-boiling solvent to the reaction vessel. Each can be recovered.
  • the collected product can be reused as it is or after appropriate processing.
  • the salt of the compound of the formula (5) obtained from the compound of the formula (4) or a salt thereof using a production method leading to the compound of the formula (5) or a salt thereof is It was found to be a dihydrochloride dihydrate of a compound of formula (5), which has been conventionally known!
  • the dihydrochloride dihydrate of the compound of the formula (5) of the present invention has better filterability than other known monohydrochlorides of the compound of the formula (5), and the crystals can be taken out by a centrifuge or the like. It will be easy.
  • the dihydrochloride dihydrate of the compound of formula (5) has good filterability, it can be obtained as a low-liquid-content, low-humidity wet substance, so that impurities can be easily removed to the filtrate side. Since it can be obtained with a high degree of purity and can be easily dried, it can be mass-produced more efficiently and is a novel substance that is more suitable for storage as an intermediate of the target compound.
  • a compound of formula (4) or a salt thereof is mixed with hydrochloric acid and acetic acid.
  • hydrochloric acid preferably 8 to 9 parts by volume
  • acetic acid preferably 2.5 parts per 1 part by weight of the compound of formula (4) or a salt thereof.
  • the total amount of hydrochloric acid and acetic acid should be about 10-12 volume parts.
  • the concentration of hydrochloric acid used at this time is usually 12% to 36%, preferably 18 to 22%.
  • the reaction is usually performed by heating to 100 ° C. or higher, preferably to the reflux temperature. If the reaction is carried out using the above specific conditions, the desired compound of the formula (5) can be obtained in a short reaction without substantially reducing the yield.
  • Another object of the present invention is to prepare a compound of the formula (4) or a salt thereof in a step of producing a compound of the formula (4) or a salt thereof from the compound of the formula (4) or a salt thereof by mixing hydrochloric acid and acetic acid.
  • the present invention provides an efficient production method suitable for industrial mass production when heated in liquid to lead to a compound of formula (5).
  • the compound of the formula (4) or a salt thereof is heated to be derivatized into the compound of the formula (5) or a salt thereof, and then the compound of the formula (5) or a salt thereof is converted to the 4 Reaction with oral benzoyl chloride provides the desired carbostyril compound of formula (1).
  • This reaction can be easily performed by a conventional amide bond formation reaction.
  • the reaction liquid is cooled, and if necessary, the reaction liquid is neutralized, and the precipitated crystals are collected by filtration to obtain a carbostyril compound. (1) or its salt can be easily separated and collected.
  • the method of the present invention can produce the carboschiri louis compound of formula (1) safely and in large quantities, and is excellent as a method for producing an industrial carbos chilly compound (1).
  • the above reaction is usually performed using a conventional base.
  • the base include alkali metal hydrogen carbonate (for example, lithium hydrogen carbonate, sodium hydrogen carbonate, potassium hydrogen carbonate, etc.), alkali metal hydroxide (for example, lithium hydroxide, sodium hydroxide, potassium hydroxide hydroxide, Cesium hydroxide, etc.), alkali metal carbonates (eg, lithium carbonate, sodium carbonate, carbonated lithium, cesium carbonate, etc.), alkali metal lower alkoxides (eg, sodium methoxide, sodium ethoxide, potassium tert-butoxide, sodium) tert-butoxide, sodium t ert pentoxide, etc.), alkali metal hydrides (eg, sodium hydride, hydrogenated) Potassium, etc.), alkali metal acetates (eg, sodium acetate, potassium acetate, etc.), trialkylamines [eg, trimethylamine, triethylamine, Nethyldiisoprop
  • the ratio of the compound of the formula (5) or a salt thereof and the 4-clobenbenzoyl chloride of the formula (6) is at least equimolar, preferably equimolar to the latter with respect to the former. 2 times mole.
  • the base should be used in an amount of at least equimolar with respect to the 4-chlorobenzoic acid lid of formula (6).
  • a conventional solvent can be used, and examples thereof include water, methanol, ethanol, propanol, butanol, acetone, acetonitrile, and ethyl acetate, one kind alone or a mixture of two or more kinds. It can also be used.
  • the above reaction is usually carried out at about ⁇ 10 to: about L00 ° C., preferably about 0 to 36 ° C., and is usually completed in about 5 minutes to 15 hours to obtain the desired carboschirily compound of formula (1). Obtainable.
  • the raw material compounds (2) to (5) in Reaction Scheme 1 may be an appropriate salt or an appropriate reactive derivative.
  • the carbostyril compound or salt thereof represented by the formula (1) of the present invention includes stereoisomers, optical isomers and solvates (hydrates, ethanolates, etc.).
  • the carbostyril compound represented by the formula (1) of the present invention can be easily converted into an acid addition salt by the action of a pharmaceutically acceptable acid, and the present invention includes this acid addition salt.
  • the acid include inorganic acids such as hydrochloric acid, sulfuric acid, phosphoric acid, hydrobromic acid, hydroiodic acid, and nitric acid, acetic acid, oxalic acid, succinic acid, maleic acid, fumaric acid, malic acid, and tartaric acid.
  • Examples include acids, citrate, malonic acid, methanesulfonic acid, benzoic acid, trifluoroacetic acid, benzenesulfonic acid, formic acid, toluenesulfonic acid and other organic acids, or amino acids (eg, alginine, aspartic acid, glutamic acid, etc.) Can do.
  • the carbostyril compound represented by the formula (1) of the present invention is a pharmaceutically acceptable base.
  • a salt can be easily formed by allowing the chemical compound to act.
  • such salts include metal salts such as alkali metal salts (for example, sodium salts and potassium salts) and alkaline earth metal salts (for example, calcium salts and magnesium salts); ammonium salts; organic base salts (For example, trimethylamine salt, triethylamine salt, pyridine salt, picolin salt, dicyclohexylamine salt, N, N, -dibenzylethylenediamine salt, etc.).
  • the basic compound include sodium hydroxide, potassium hydroxide, calcium hydroxide, sodium carbonate, potassium hydrogen carbonate and the like.
  • the carbostyril compound represented by the formula (1) of the present invention is more efficiently absorbed into the living body by reducing the particle diameter with a normal pulverizer (for example, an atomizer). It can be carried out.
  • a normal pulverizer for example, an atomizer
  • the particle size can be easily reduced by a known method well known to those skilled in the art.
  • the method can be refined by a ceramic mill under suitable conditions such as the mill rotation ratio or the feed ratio of the carboschilli compound (1). It can also be refined by passing through an air jet mill with an appropriate supply air pressure while rotating at an appropriate supply ratio or rotation ratio of the carboschilli compound represented by the formula (1) of the present invention. Is possible.
  • the danger of bumping can be avoided by using a high-boiling solvent, so that a desired carbostyril compound or salt thereof of the formula (1) can be produced safely,
  • the volumetric efficiency of the reactor can be greatly increased, which is extremely effective for mass synthesis.
  • the high-boiling solvent used is easily recovered by distilling off during the reaction, or by separating the liquid after distilling off the reaction.
  • the acid (hydrochloric acid) filtrate after solid-liquid separation can be reused without discarding the majority of the fractions except the initial fraction by performing a simple distillation operation. Since it can be recovered as (hydrochloric acid), adverse effects on the environment can be reduced.
  • the post-treatment after completion of the reaction can obtain the compound of formula (5) or a salt thereof in a high yield by a simple operation of crystal filtration after cooling. It is effective for the large-scale synthesis of the carboschiril compound of formula (1) or a salt thereof.
  • the dihydrochloride dihydrate of the compound of the formula (5) of the present invention is crystallized by a centrifuge or the like, which has better filterability than other known monohydrochlorides of the compound of the formula (5). It becomes easy to take out.
  • the dihydrochloride dihydrate of the compound of formula (5) has good filterability, it can be obtained as a low-liquid-content, low-humidity wet substance, so that impurities can be easily removed to the filtrate side. Since it can be obtained with a high degree of purity and can be easily dried, it can be mass-produced more efficiently and is a novel substance that is more suitable for storage as an intermediate of the target compound.
  • the compound of the formula (4) or a salt thereof As another production method leading from the compound of the formula (4) or a salt thereof to the compound of the formula (5) or a salt thereof, the compound of the formula (4) or By heating the salt in a mixture of hydrochloric acid and acetic acid at a certain ratio, the increase in the interface due to foaming can be suppressed to an acceptable level in industrial mass production without adding a high-boiling solvent. In addition, the reaction can be completed in a relatively short time.

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Abstract

Disclosed is an improved process which can produce a carbostyril compound of the formula (1) or a salt thereof, which is useful as a pharmaceutical agent, more safely with higher efficiency. An improved process for producing a carbostyril compound comprising the steps of adding a high boiling solvent to a compound of the formula (4) and refluxing the resulting mixture under heating in hydrochloric acid to produce a compound of the formula (5) safely and acylating the compound of the formula (5) to produce a carbostyril compound of the formula (1).

Description

カルボスチリル化合物の製造法  Method for producing carbostyril compound
技術分野  Technical field
[0001] 本件は、胃潰瘍等の治療剤として有用な下記のカルボスチリルイ匕合物をより安全に かつ効率よく製造するカルボスチリル化合物の改良製造法に関する。  [0001] The present invention relates to an improved method for producing a carbostyril compound, which produces the following carbostyril compound which is useful as a therapeutic agent for gastric ulcer and the like more safely and efficiently.
背景技術  Background art
[0002] 本発明のカルボスチリルイ匕合物は、下記式(1)で示されるカルボスチリルイ匕合物( 化学名: 2—(4 クロ口べンゾィルァミノ) - 3- [2 (1Η)ーキノリノンー4 ィル]プロ ピオン酸)であって、胃潰瘍、急性胃炎、または慢性胃炎の急性悪化期に現れる胃 粘膜病変に対する優れた治療効果を示す薬剤である。  [0002] The carboschirirui compound of the present invention is a carboschirirui compound represented by the following formula (1) (chemical name: 2— (4 black benzoylamino)-3- [2 (1Η) -quinolinone 4-yl] propionic acid), a drug that exhibits excellent therapeutic effects on gastric mucosal lesions appearing during gastric ulcer, acute gastritis, or acute exacerbation of chronic gastritis.
[0003] [化 1]  [0003] [Chemical 1]
Figure imgf000003_0001
Figure imgf000003_0001
[0004] 本発明の式(1)で示されるカルボスチリルイ匕合物の製造方法としては、例えば下記 反応式 1に示す方法が知られている (特許文献 1)。すなわち、式 (2)の化合物をナト リウムエトキシド等の塩基の存在下に式 (3)の化合物と反応させて式 (4)の化合物を 得、この化合物を塩酸等の鉱酸で加水分解及び脱炭酸させて式 (5)の化合物を製 造した後、式 (6)の 4 クロ口べンゾイルクロリドでァシルイ匕させて目的とする式(1)の 化合物を製造する。  [0004] As a method for producing a carbostyril compound represented by the formula (1) of the present invention, for example, a method represented by the following reaction formula 1 is known (Patent Document 1). That is, the compound of formula (2) is reacted with the compound of formula (3) in the presence of a base such as sodium ethoxide to obtain the compound of formula (4), and this compound is hydrolyzed with a mineral acid such as hydrochloric acid. And decarboxylating to produce the compound of formula (5), and then saponifying with 4-chlorobenzoyl chloride of formula (6) to produce the desired compound of formula (1).
[0005] [化 2] 反応式 1 [0005] [Chemical 2] Reaction formula 1
Figure imgf000004_0001
Figure imgf000004_0001
上記の方法にぉ 、て、式 (4)の化合物から式(5)の化合物を製造する工程は、化 合物 (4)を、例えば 20%塩酸中で加熱還流させる必要がある力 この反応工程では 、反応の進行に伴いエタノール、炭酸ガス、酢酸、及び酢酸ェチルが副生する。その ため、発生する炭酸ガスにより反応界面が激しく泡立ち、し力もこの泡はすぐには消 失しない。特に化合物 (4)に対する塩酸の量が少ない場合には、この泡による界面 の急激な上昇が認められ、還流を継続して行うことがしばしば困難となる。しかも、そ のような泡による界面の急激な上昇は突沸の危険を伴うため、目的物のカルボスチリ ル化合物(1)を大量に製造する場合、安全性が大きな問題となる。また、かかる発泡 を避けるには加熱を抑える必要があり、その反応を促進するために必要な熱を充分 にかけられない。さらに上記反応工程で副生するエタノール、酢酸ェチル等により還 流温度が低下し、反応速度の遅延誘因となる問題が生じる。したがって、この化合物 (4)力 化合物(5)に導く工程をいかに安全にかつ効率よく行うことが本発明の式(1 )で示されるカルボスチリルイ匕合物の工業的製造上重要な要素となって 、る。  According to the above method, the step of producing the compound of the formula (5) from the compound of the formula (4) is required to heat and reflux the compound (4) in, for example, 20% hydrochloric acid. In the process, ethanol, carbon dioxide, acetic acid, and ethyl acetate are by-produced as the reaction proceeds. For this reason, the reaction interface is bubbling violently due to the generated carbon dioxide gas, and this foam does not disappear immediately. In particular, when the amount of hydrochloric acid relative to compound (4) is small, a rapid increase in the interface due to the bubbles is observed, and it is often difficult to carry out the refluxing continuously. In addition, the sudden rise of the interface caused by such bubbles involves the risk of bumping, and safety is a major problem when producing the target carbostyryl compound (1) in large quantities. Moreover, in order to avoid such foaming, it is necessary to suppress heating, and the heat necessary to accelerate the reaction cannot be sufficiently applied. In addition, ethanol, ethyl acetate and the like by-produced in the above reaction step lower the reflux temperature, causing a problem that causes a delay in the reaction rate. Therefore, how to safely and efficiently carry out the process leading to this compound (4) force compound (5) is an important factor in the industrial production of the carboschiril compound represented by the formula (1) of the present invention. Become.
特許文献 1 :特開昭 60— 19767号公報 Patent Document 1: Japanese Patent Application Laid-Open No. 60-19767
発明の開示 発明が解決しょうとする課題 Disclosure of the invention Problems to be solved by the invention
[0007] しかして、上記従来法における式 (4)の化合物またはその塩力 式(5)の化合物ま たはその塩を製造する工程において、発泡による界面の上昇を抑え、大量合成する 場合でも安全に効率よく製造できる方法を見出すべく種々検討した結果、その反応 に際して、特定の物質を反応系に添加することによって発泡を抑え、より安全に有用 な化合物(5)またはその塩を効率よく製造でき、っ 、でその化合物(5)またはその塩 をァシルイ匕に付すことにより所望の式(1)のカルボスチリルイ匕合物またはその塩が得 られることを見出し、本発明を完成するに至った。  [0007] Therefore, in the process of producing the compound of the formula (4) or the salt power of the formula (5) or the salt thereof in the above conventional method, even when a large amount is synthesized by suppressing the rise of the interface due to foaming. As a result of various investigations to find a method that can be safely and efficiently produced, by adding a specific substance to the reaction system during the reaction, foaming is suppressed and the safer and useful compound (5) or a salt thereof is efficiently produced. Thus, it was found that by subjecting the compound (5) or a salt thereof to an acylate, a desired carbostyril compound of the formula (1) or a salt thereof can be obtained, and the present invention was completed. It was.
[0008] 本発明の目的は、医薬として有用な式(1)のカルボスチリルイ匕合物またはその塩を より安全に効率よく製造できる改善された方法を提供することである。  [0008] An object of the present invention is to provide an improved method by which a carbostyril compound of formula (1) or a salt thereof useful as a medicament can be produced more safely and efficiently.
また本発明の製造法において中間体として製造される式(5)の化合物またはその 塩は、所望の式(1)のカルボスチリルイ匕合物またはその塩を製造するための中間体 物質として、反応系からの結晶の取り出しがより容易かつ簡便に行えることが望まれ る。また、所望の式(1)のカルボスチリルイ匕合物またはその塩を製造するための中間 体物質として、保存に好適であるためには、その乾燥がより容易に効率よく行えること が望まれる。  In addition, the compound of formula (5) or a salt thereof produced as an intermediate in the production method of the present invention is an intermediate substance for producing a desired carbostyril compound or a salt thereof of formula (1). It is desired that the crystal can be easily and easily removed from the reaction system. Moreover, in order to be suitable for storage as an intermediate substance for producing a desired carboschiril compound of the formula (1) or a salt thereof, it is desired that the drying can be performed more easily and efficiently. .
[0009] 本発明の他の目的は、式(2)の化合物またはその塩からの目的の式(1)のカルボ スチリルイ匕合物またはその塩を製造する一連の工程中、式 (4)の化合物またはその 塩から式(5)の化合物またはその塩を製造する工程にぉ 、て、本工程に適した高沸 点溶剤存在中に加熱することにより、反応途中に発生する泡によって引き起こされる 急激な界面の上昇およびこれに伴う突沸を抑制し、もって、 目的とするカルボスチリ ル化合物 (式(1) )またはその塩をより安全に製造する方法を提供するものである。 本発明のもう一つの目的は、上記の突沸予防の問題を改善しつつ、必要に応じて 反応工程におけるエタノール、酢酸ェチル等の副生物を除去しながら還流温度を維 持することにより、式 (5)の化合物またはその塩をより効率よく製造する方法をも提供 するものである。  Another object of the present invention is to provide a compound of the formula (4) during a series of steps for producing the desired carbostyril compound of the formula (1) or a salt thereof from the compound of the formula (2) or a salt thereof. In the process of producing a compound of the formula (5) or a salt thereof from the compound or a salt thereof, heating in the presence of a high-boiling point solvent suitable for this step causes a sudden reaction caused by bubbles generated during the reaction. The present invention provides a method for more safely producing the desired carbostyryl compound (formula (1)) or a salt thereof by suppressing the rise of the interface and bumping accompanying this. Another object of the present invention is to improve the above-mentioned problem of preventing bumping, while maintaining the reflux temperature while removing by-products such as ethanol and ethyl acetate in the reaction step as necessary. The present invention also provides a method for producing the compound 5) or a salt thereof more efficiently.
さらに本発明の目的は、上記所望の中間体として式(5)の化合物の二塩酸塩二水 和物を提供するものである。 課題を解決するための手段 A further object of the present invention is to provide a dihydrochloride dihydrate of the compound of formula (5) as the desired intermediate. Means for solving the problem
[0010] 本発明によれば、酸性条件下、高沸点溶剤存在中、式 (4)の化合物またはその塩 を加熱させることにより、安全に式(5)の化合物またはその塩を製造することができ、 必要に応じて反応工程におけるエタノール、酢酸ェチル等の副生物を除去しながら 加熱温度、特に還流温度を維持することにより、式 (5)の化合物またはその塩をさら に効率よく製造することができる。次いで、その化合物(5)またはその塩を式 (6)の 4 クロ口べンゾイルクロリドでァシルイ匕させることにより、目的とする式(1)のカルボス チリル化合物またはその塩を得ることができる。  [0010] According to the present invention, the compound of formula (5) or a salt thereof can be produced safely by heating the compound of formula (4) or a salt thereof in the presence of a high-boiling solvent under acidic conditions. The production of the compound of formula (5) or a salt thereof can be carried out more efficiently by maintaining the heating temperature, particularly the reflux temperature, while removing by-products such as ethanol and ethyl acetate in the reaction step as necessary. Can do. Subsequently, the compound (5) or a salt thereof is acylated with 4 chlorobenzoyl chloride of the formula (6) to obtain the target carbostyryl compound of the formula (1) or a salt thereof.
[0011] すなわち、本発明によれば、式 (4)の化合物またはその塩を酸性条件下に加熱さ せて式 (5)の化合物またはその塩を導くに際し、特定の高沸点溶剤と共に反応を行 うことにより、高沸点溶剤が消泡剤として機能し、望ましくない発泡を抑え、充分なカロ 熱を加えて反応を促進することができる。  That is, according to the present invention, when the compound of the formula (4) or a salt thereof is heated under acidic conditions to derive the compound of the formula (5) or a salt thereof, the reaction is performed with a specific high boiling point solvent. By doing so, the high boiling point solvent functions as an antifoaming agent, suppresses undesirable foaming, and adds sufficient caloric heat to accelerate the reaction.
[0012] この式 (4)の化合物またはその塩力 式(5)の化合物またはその塩に導く反応では 、また、反応の進行に伴い、エタノール、酢酸ェチル等の比較的低沸点の物質が副 生するため、そのまま、反応を継続すると加熱温度、特に還流温度が下がり、充分な 熱が加えられないため反応が遅延する原因となる。したがって、力かる副生する低沸 点物質を反応系外に抜き取り反応効率を維持する必要がある。本発明によれば、加 熱温度、特に還流温度を維持し反応効率を高めるために発泡の問題を改善しつつ、 必要に応じて反応工程における副生物を除去しながら該温度を維持することにより、 式 (5)の化合物またはその塩をより効率よく製造する方法を提供することができる。  [0012] In the reaction leading to the compound of the formula (4) or a salt power thereof, or to the compound of the formula (5) or a salt thereof, a substance having a relatively low boiling point such as ethanol or ethyl acetate is added as the reaction proceeds. Therefore, if the reaction is continued as it is, the heating temperature, particularly the reflux temperature is lowered, and the reaction is delayed because sufficient heat cannot be applied. Therefore, it is necessary to maintain the reaction efficiency by extracting the low-boiling point substances generated as a by-product from the reaction system. According to the present invention, by maintaining the heating temperature, particularly the reflux temperature and improving the efficiency of the reaction to improve the foaming problem, the temperature is maintained while removing by-products in the reaction process as necessary. A method for producing the compound of the formula (5) or a salt thereof more efficiently can be provided.
[0013] 本発明によれば、式 (4)の化合物またはその塩を加熱して、式(5)の化合物または その塩を得る工程が水中で行われ、および Zまたは、式(5)の化合物またはその塩 をァシル化させることにより目的とする式(1)のカルボスチリルイ匕合物またはその塩を 得る反応工程力 水中もしくは有機溶媒中またはその混合液中で行われる前記式(5 )の化合物またはその塩、または式(1)のカルボスチリルイ匕合物またはその塩の製造 法を提供することができる。  [0013] According to the present invention, the step of heating the compound of the formula (4) or a salt thereof to obtain the compound of the formula (5) or a salt thereof is performed in water, and Z or of the formula (5) Reaction process power to obtain a target carbostyril compound of the formula (1) or a salt thereof by subjecting the compound or a salt thereof to acylation The above formula (5) carried out in water, an organic solvent or a mixture thereof Or a salt thereof, or a method for producing a carbostyril compound of the formula (1) or a salt thereof.
[0014] さらに本発明によれば、式 (4)の化合物またはその塩を加熱して、式(5)の化合物 またはその塩を得る工程において、塩酸の存在中で加熱反応が行われる式(5)の化 合物またはその塩の製造法を提供することができる。 [0014] Further, according to the present invention, in the step of heating the compound of the formula (4) or a salt thereof to obtain the compound of the formula (5) or a salt thereof, a reaction in which the heating reaction is carried out in the presence of hydrochloric acid ( 5) A method for producing a compound or a salt thereof can be provided.
[0015] また、本発明によれば、式 (4)の化合物またはその塩を加熱して、式(5)の化合物 またはその塩を得る工程に用いられる高沸点溶剤がノルマルォクタノールおよび Zま たはァセトフエノンである式(5)の化合物またはその塩の製造法が提供できる。  [0015] According to the present invention, the high boiling point solvent used in the step of heating the compound of the formula (4) or a salt thereof to obtain the compound of the formula (5) or a salt thereof is normal octanol and Z Alternatively, it is possible to provide a method for producing a compound of formula (5) or a salt thereof which is aacetophenone.
[0016] 本発明によれば、本発明の上記製造法によって得られる式(5)の化合物またはそ の塩が、式 (5)で示される化合物の二塩酸塩二水和物であることを特徴とする新規 物質を提供することができる。  [0016] According to the present invention, the compound of the formula (5) or a salt thereof obtained by the production method of the present invention is a dihydrochloride dihydrate of the compound represented by the formula (5). It is possible to provide new substances with features.
[0017] 本発明で用いられる高沸点溶剤としては、上記のような操作を支障なく行うことので きる物質であればよい。  [0017] The high boiling point solvent used in the present invention may be any substance that can perform the above-described operation without any trouble.
し力して本発明者らによる工業的レベルの物質製造法の研究によれば、該溶剤とし ては上記炭酸ガスの発生に起因する発泡による界面の上昇を抑制し得る物質であつ て、且つその反応に用いられる酸を加えた溶媒と共沸し、酸を加えた溶媒よりも比重 力 、さぐ酸を加えた溶媒と混じり合わずに分離し、酸を加えた溶媒より高沸点である ことがその目的に適していることを見出した。  However, according to the study of the industrial level production method by the present inventors, the solvent is a substance that can suppress the rise of the interface due to foaming caused by the generation of the carbon dioxide gas, and It must azeotrope with the solvent added with the acid used in the reaction, have a higher specific gravity than the solvent added with the acid, and be separated without mixing with the solvent added with the acid, and have a higher boiling point than the solvent added with the acid. Has been found to be suitable for that purpose.
[0018] 本発明者らは、特に後記実施例において示されるように本発明の製造法において 用いられる酸としては、塩酸が好ましく例示でき、対応する高沸点溶剤としては、例え ば塩酸よりも比重が小さぐ塩酸と混じり合わな 、高沸点物質であるノルマルオタタノ ールおよび Zまたはァセトフヱノンがよりその目的に適していることを見出した。  [0018] The inventors of the present invention can preferably illustrate hydrochloric acid as the acid used in the production method of the present invention, as shown in the examples below, and the corresponding high-boiling solvent has a specific gravity higher than that of hydrochloric acid, for example. It has been found that normal otatanol and Z or acetophenone, which are high-boiling substances that are not mixed with small hydrochloric acid, are more suitable for that purpose.
発明を実施するための最良の形態  BEST MODE FOR CARRYING OUT THE INVENTION
[0019] 本発明にお 、て、式 (4)の化合物またはその塩を酸加水分解して式(5)の化合物 またはその塩に導く反応は、加水分解触媒の存在下、高沸点溶剤を添加して行われ る。加水分解触媒としては、塩酸、臭化水素酸、ヨウ化水素酸などのハロゲンィ匕水素 酸、硫酸、リン酸などの鉱酸類、ギ酸、酢酸、トリフルォロ酢酸、 p—トルエンスルホン 酸等の有機酸を例示でき、特に好ましい触媒としては、塩酸を例示できる。  In the present invention, the reaction leading to the compound of formula (4) or a salt thereof by acid hydrolysis to the compound of formula (5) or a salt thereof is carried out by using a high-boiling solvent in the presence of a hydrolysis catalyst. It is done by adding. Hydrolysis catalysts include halogen hydrofluoric acids such as hydrochloric acid, hydrobromic acid and hydroiodic acid, mineral acids such as sulfuric acid and phosphoric acid, and organic acids such as formic acid, acetic acid, trifluoroacetic acid and p-toluenesulfonic acid. As a particularly preferable catalyst, hydrochloric acid can be exemplified.
これらの触媒は、 1種単独でまたは 2種以上混合して用いることもできる。また該反 応の溶媒を上記の酸を溶解している水等の溶媒で兼ねてもよぐ塩酸に含まれてい る水が該反応の溶媒として特に好ま 、。  These catalysts can be used singly or in combination of two or more. In addition, water contained in hydrochloric acid, which may be used as the reaction solvent with a solvent such as water in which the acid is dissolved, is particularly preferred as the solvent for the reaction.
触媒としての酸の使用量は、特に限定はされないが、例えば酸として塩酸を使用す る場合においては、該反応の溶媒を兼ねてこれを使用することができ、通常、濃度がThe amount of acid used as the catalyst is not particularly limited. For example, hydrochloric acid is used as the acid. In this case, it can also be used as a solvent for the reaction, and the concentration is usually
12〜36%、好ましくは 18〜22%の塩酸を、式 (4)の化合物またはその塩 1重量部 に対して、通常 6容量部以上、好ましくは 8容量部以上用いるとよい。 12 to 36%, preferably 18 to 22% of hydrochloric acid is usually used in an amount of 6 parts by volume or more, preferably 8 parts by volume or more based on 1 part by weight of the compound of the formula (4) or a salt thereof.
[0020] 本発明にお 、て使用され得る高沸点溶剤としては、上記式 (4)の化合物またはそ の塩を酸性条件下で加熱反応する工程において副生する炭酸ガスの発生に起因す る発泡による界面の上昇を抑制し得る (消泡効果を有する)物質として存在する(添カロ されることを含む)ものであって、酸を加えた溶媒と混じり合わず、かつその反応に用 いられる酸を加えた溶媒と共沸し、酸を加えた溶媒よりも高沸点であることおよび低 比重であることを満足する物理ィ匕学的特性を有する物質であれば、特に限定されな い。高沸点溶剤としてより具体的には、例えばノルマルペンタノール、 2—ペンタノ一 ル、 3 ペンタノール、 3—メチルー 1ーブタノール、ノルマルへキサノール、 2—メチ ルー 1 ペンタノール、 2 ェチルー 1ーブタノール、 3 へプタノール、ノルマルオタ タノール、ノルマルノナノール、 3, 5, 5 トリメチルー 1一へキサノール、ノルマルデ 力ノール、ノルマルゥンデ力ノール、ノルマルドデカノールなどの炭素数 5〜 12のアル コール、ァセトフエノン、ォクチル酸、テトラリン、クメンなどが挙げられ、例えば、塩酸 を該反応の酸触媒および溶媒を兼ねて使用する場合には、前記の条件を満足する 物理ィ匕学的特性を有する、ノルマルォクタノールおよびァセトフエノンをより好適な高 沸点溶剤として用いることができる。  [0020] The high boiling point solvent that can be used in the present invention results from the generation of carbon dioxide gas by-produced in the step of heating and reacting the compound of the above formula (4) or a salt thereof under acidic conditions. It exists as a substance (including defoaming effect) that can suppress the rise of the interface due to foaming (including defoaming), does not mix with the solvent to which the acid is added, and is used for the reaction. There is no particular limitation as long as it is a substance that has physico-chemical properties that azeotropes with the solvent to which the acid is added and has a higher boiling point and lower specific gravity than the solvent to which the acid is added. . More specific examples of the high boiling point solvent include normal pentanol, 2-pentanol, 3-pentanol, 3-methyl-1-butanol, normal hexanol, 2-methyl-1-pentanol, 2-ethyl-1-butanol, and 3 Ptanol, normal otathanol, normal nonanol, 3, 5, 5 trimethyl- 1 hexanol, normalde force norm, normalunde force norl, normal dodecanol etc. For example, when hydrochloric acid is used also as an acid catalyst and a solvent for the reaction, normaloctanol and acetophenone having physical and physical properties satisfying the above conditions are more suitable. It can be used as a high boiling point solvent.
高沸点溶剤の使用量は特に限定はされず、発泡の程度、反応缶の形状などに応じ て好適な使用量は変動するが、式 (4)の化合物またはその塩 1重量部に対して、通 常、 0. 1〜3容量部程度、好ましくは 0. 15〜1容量部程度の範囲力も選ばれる。 上記反応は、通常 80°Cから反応溶媒の還流温度に加熱、好ましくは 100°C力 反 応溶媒の還流温度に加熱して行い、通常 6〜24時間程度で完了する。  The amount of the high-boiling solvent used is not particularly limited, and the preferred amount varies depending on the degree of foaming, the shape of the reaction vessel, etc., but with respect to 1 part by weight of the compound of formula (4) or a salt thereof, Usually, a range force of about 0.1 to 3 parts by volume, preferably about 0.1 to 1 parts by volume is also selected. The above reaction is usually carried out by heating from 80 ° C. to the reflux temperature of the reaction solvent, preferably 100 ° C. and the reaction solvent, and is usually completed in about 6 to 24 hours.
[0021] 本発明の製造法に用いられる高沸点溶剤は、酸性条件下において式 (4)の化合 物またはその塩を加熱反応させる工程にぉ 、て、反応液界面の上昇を抑制する効 果があり、安全に式(5)の化合物またはその塩を製造することができるうえ、反応缶の 容積効率も格段に高めることができるので、式(5)の化合物またはその塩の大量合 成に好適に使用できる。本発明において、式 (4)の化合物またはその塩から、式(5) の化合物またはその塩に導く反応は、必要に応じて反応工程における副生物を除去 しながら加熱温度、特に還流温度を維持することにより、式 (5)の化合物またはその 塩をさらに効率よく製造することができる。 [0021] The high-boiling solvent used in the production method of the present invention has the effect of suppressing an increase in the reaction liquid interface in the step of heating and reacting the compound of formula (4) or a salt thereof under acidic conditions. Since the compound of formula (5) or a salt thereof can be produced safely and the volumetric efficiency of the reactor can be greatly increased, it can be used for mass synthesis of the compound of formula (5) or a salt thereof. It can be suitably used. In the present invention, from the compound of the formula (4) or a salt thereof, the compound of the formula (5) In the reaction leading to the compound or its salt, the compound of the formula (5) or its salt is more efficiently produced by maintaining the heating temperature, particularly the reflux temperature while removing by-products in the reaction step as necessary. be able to.
該反応を、例えばディーン 'スターク装置を使用して行えば、上記の 2つの条件は 同時に満たすことができ、工業的製造方法として好適に使用できる。  If the reaction is performed using, for example, a Dean's Stark apparatus, the above two conditions can be satisfied at the same time, which can be suitably used as an industrial production method.
即ち、具体的には、還流温度において、共沸した水と高沸点溶剤の凝縮液は、該 装置内で二層に分離し、本発明の製造法に用いられる高沸点溶剤は上層に、副生 する低沸点物質は下層(水層;例えば塩酸)に分配される。したがって、下層のみを 少量ずつ抜き取ることにより、低沸点物質は反応系外へ除かれ、必要な高い還流温 度が維持されて反応遅延が避けられると共に、上層の高沸点溶剤のみを反応槽に 循環して用いることができ、発泡による界面の上昇を継続して抑制することができる。 なお、反応が終了したのちは、高沸点溶剤を反応槽に循環させずに、凝縮液を反 応系外へ抜き取り、これを分液することによって、高沸点溶剤と水 (酸を含む)をそれ ぞれ回収することができる。また、この回収品はそのまま、あるいは適当な処理を行つ たのちに再使用することができる。  Specifically, at the reflux temperature, the azeotropic water and high-boiling point solvent condensate are separated into two layers in the apparatus, and the high-boiling point solvent used in the production method of the present invention is separated into the upper layer. The resulting low-boiling substances are distributed to the lower layer (aqueous layer; eg hydrochloric acid). Therefore, by extracting only the lower layer little by little, low-boiling substances are removed from the reaction system, the necessary high reflux temperature is maintained and reaction delay is avoided, and only the upper-boiling solvent in the upper layer is circulated to the reaction tank. And the rise of the interface due to foaming can be continuously suppressed. After completion of the reaction, the high-boiling solvent and water (including acid) are removed by extracting the condensate out of the reaction system and separating it without circulating the high-boiling solvent to the reaction vessel. Each can be recovered. In addition, the collected product can be reused as it is or after appropriate processing.
[0022] 本発明にお 、て、式 (4)の化合物またはその塩から、式(5)の化合物またはその塩 に導く製造法を用いて得られた式(5)の化合物の塩は、従来知られて!/、な 、新規物 質である式(5)の化合物の二塩酸塩二水和物であると判明した。 In the present invention, the salt of the compound of the formula (5) obtained from the compound of the formula (4) or a salt thereof using a production method leading to the compound of the formula (5) or a salt thereof is It was found to be a dihydrochloride dihydrate of a compound of formula (5), which has been conventionally known!
本発明の式(5)の化合物の二塩酸塩二水和物は、他の公知の式(5)の化合物の 一塩酸塩と比べると濾過性が良ぐ遠心分離機等による結晶の取り出しが容易となる 。また、式(5)の化合物の二塩酸塩二水和物は、濾過性が良いことから含液率の低 V、湿体として得ることができるため、不純物が濾液側に除去され易くより高純度で得 ることができ、さらには乾燥が容易となることから、より効率的な大量製造を行うことが でき、目的化合物の中間体としてより保存に好適な新規物質である。  The dihydrochloride dihydrate of the compound of the formula (5) of the present invention has better filterability than other known monohydrochlorides of the compound of the formula (5), and the crystals can be taken out by a centrifuge or the like. It will be easy. In addition, since the dihydrochloride dihydrate of the compound of formula (5) has good filterability, it can be obtained as a low-liquid-content, low-humidity wet substance, so that impurities can be easily removed to the filtrate side. Since it can be obtained with a high degree of purity and can be easily dried, it can be mass-produced more efficiently and is a novel substance that is more suitable for storage as an intermediate of the target compound.
[0023] また、式 (4)の化合物またはその塩から、式(5)の化合物またはその塩に導く別の 製造法として、式 (4)の化合物またはその塩を、塩酸および酢酸の混合液中で加熱 して式(5)の化合物に導く場合、これらの使用割合によつては、高沸点溶剤を添加せ ずとも、発泡による界面上昇は、工業的な大量製造において許容できる程度まで抑 えられ、また比較的短時間に反応を完結させることができることを見出した。具体的に は、式 (4)の化合物またはその塩 1重量部に対して、塩酸を 5〜9容量部、好ましくは 8〜9容量部、酢酸を 2〜5容量部、好ましくは 2. 5〜3. 5容量部とし、さらに、塩酸と 酢酸の合計量を 10〜 12容量部程度とすればよい。尚、この時使用する塩酸の濃度 は、通常 12%〜36%、好ましくは 18〜22%である。該反応は、通常 100°C以上に 加熱して、好ましくは還流温度に加熱して行う。以上の特定条件を用いて該反応を 行えば、短時間の反応で、収率をほとんど低下させることなぐ所望の式(5)の化合 物を得ることができる。 [0023] As another production method for deriving a compound of formula (4) or a salt thereof from a compound of formula (5) or a salt thereof, a compound of formula (4) or a salt thereof is mixed with hydrochloric acid and acetic acid. When heated to the compound of formula (5), the increase in the interface due to foaming is suppressed to an acceptable level in industrial mass production without adding a high-boiling solvent. It was also found that the reaction can be completed in a relatively short time. Specifically, 5 to 9 parts by volume of hydrochloric acid, preferably 8 to 9 parts by volume, and 2 to 5 parts by volume of acetic acid, preferably 2.5 parts per 1 part by weight of the compound of formula (4) or a salt thereof. ~ 3.5 volume parts, and the total amount of hydrochloric acid and acetic acid should be about 10-12 volume parts. The concentration of hydrochloric acid used at this time is usually 12% to 36%, preferably 18 to 22%. The reaction is usually performed by heating to 100 ° C. or higher, preferably to the reflux temperature. If the reaction is carried out using the above specific conditions, the desired compound of the formula (5) can be obtained in a short reaction without substantially reducing the yield.
また、本発明の目的は、式 (4)の化合物またはその塩から、式(5)の化合物または その塩を製造する工程において、式 (4)の化合物またはその塩を、塩酸および酢酸 の混合液中で加熱して式 (5)の化合物に導く場合の、工業的大量生産に適した、効 率的な製造方法を提供するものである。  Another object of the present invention is to prepare a compound of the formula (4) or a salt thereof in a step of producing a compound of the formula (4) or a salt thereof from the compound of the formula (4) or a salt thereof by mixing hydrochloric acid and acetic acid. The present invention provides an efficient production method suitable for industrial mass production when heated in liquid to lead to a compound of formula (5).
さらに本発明において、式 (4)の化合物またはその塩を加熱して、式(5)の化合物 またはその塩に誘導した後、式(5)の化合物またはその塩を式 (6)の 4 クロ口ベン ゾイルク口リドと反応させて所望の式(1)のカルボスチリル化合物を得る。この反応は 常法のアミド結合生成反応によって容易に行うことができる。また、用いる溶媒を適当 に選択することによって、反応終了後、反応液を冷却し、また、必要に応じて反応液 を中和し、析出する結晶を濾取することによりカルボスチリルイ匕合物(1)またはその塩 を簡単に分離採取することができる。  Furthermore, in the present invention, the compound of the formula (4) or a salt thereof is heated to be derivatized into the compound of the formula (5) or a salt thereof, and then the compound of the formula (5) or a salt thereof is converted to the 4 Reaction with oral benzoyl chloride provides the desired carbostyril compound of formula (1). This reaction can be easily performed by a conventional amide bond formation reaction. In addition, by appropriately selecting the solvent to be used, after completion of the reaction, the reaction liquid is cooled, and if necessary, the reaction liquid is neutralized, and the precipitated crystals are collected by filtration to obtain a carbostyril compound. (1) or its salt can be easily separated and collected.
したがって、本発明方法は、式(1)のカルボスチリルイ匕合物を安全かつ大量に製造 することができ、工業的なカルボスチリルイ匕合物(1)の製法として優れて 、る。  Accordingly, the method of the present invention can produce the carboschiri louis compound of formula (1) safely and in large quantities, and is excellent as a method for producing an industrial carbos chilly compound (1).
上記反応は、通常、慣用の塩基を用いて行う。塩基としては例えば炭酸水素アル力 リ金属 (例えば、炭酸水素リチウム、炭酸水素ナトリウム、炭酸水素カリウム等)、アル カリ金属水酸化物(例えば、水酸化リチウム、水酸化ナトリウム、水酸ィ匕カリウム、水酸 化セシウム等)、炭酸アルカリ金属 (例えば、炭酸リチウム、炭酸ナトリウム、炭酸力リウ ム、炭酸セシウム等)、アルカリ金属低級アルコキシド (例えば、ナトリウムメトキシド、 ナトリウムエトキシド、カリウム tert—ブトキシド、ナトリウム tert—ブトキシド、ナトリウム t ert ペントキシド等)、アルカリ金属水素化合物(例えば、水素化ナトリウム、水素化 カリウム等)、アルカリ金属の酢酸塩 (例えば、酢酸ナトリウム、酢酸カリウム等)、トリア ルキルアミン [例えば、トリメチルァミン、トリェチルァミン、 N ェチルジイソプロピルァ ミン等]、ピリジン、キノリン、ピぺリジン、イミダゾール、ピコリン、ジメチルァミノピリジン 、ジメチルァ-リン、 N—メチルモルホリン、 1, 5 ジァザビシクロ [4. 3. 0]ノン一 5— ェン(DBN)、 1, 4ージァザビシクロ [2. 2. 2]オクタンー5—ェン(0八 じ0)、 1, 8 —ジァザビシクロ [5. 4. 0]ゥンデ力— 7 ェン(DBU)等が例示できる。これらの塩 基は、 1種単独または 2種以上混合して使用することもできる。 The above reaction is usually performed using a conventional base. Examples of the base include alkali metal hydrogen carbonate (for example, lithium hydrogen carbonate, sodium hydrogen carbonate, potassium hydrogen carbonate, etc.), alkali metal hydroxide (for example, lithium hydroxide, sodium hydroxide, potassium hydroxide hydroxide, Cesium hydroxide, etc.), alkali metal carbonates (eg, lithium carbonate, sodium carbonate, carbonated lithium, cesium carbonate, etc.), alkali metal lower alkoxides (eg, sodium methoxide, sodium ethoxide, potassium tert-butoxide, sodium) tert-butoxide, sodium t ert pentoxide, etc.), alkali metal hydrides (eg, sodium hydride, hydrogenated) Potassium, etc.), alkali metal acetates (eg, sodium acetate, potassium acetate, etc.), trialkylamines [eg, trimethylamine, triethylamine, Nethyldiisopropylamine, etc.], pyridine, quinoline, piperidine, imidazole, Picoline, dimethylaminopyridine, dimethylamino, N-methylmorpholine, 1,5 diazabicyclo [4.3.0] non-one (DBN), 1,4-diazabicyclo [2.2.2] octane-5 —Yen (0 8 0), 1, 8 —Jazabicyclo [5. 4. 0] Wunde force—7 Yen (DBU). These base groups can be used alone or in combination of two or more.
上記反応にお 、て、式(5)の化合物またはその塩と式(6)の 4 クロ口べンゾイルク 口リドの使用割合は、前者に対して、後者を少なくとも等モル、好ましくは等モル〜 2 倍モルとする。また、塩基の使用割合は、式 (6)の 4 クロ口べンゾイルク口リドに対し て、少なくとも等モル以上を用いる。  In the above reaction, the ratio of the compound of the formula (5) or a salt thereof and the 4-clobenbenzoyl chloride of the formula (6) is at least equimolar, preferably equimolar to the latter with respect to the former. 2 times mole. In addition, the base should be used in an amount of at least equimolar with respect to the 4-chlorobenzoic acid lid of formula (6).
上記反応に用いられる溶媒としては、慣用の溶媒を用いることができ、水、メタノー ル、エタノール、プロパノール、ブタノール、アセトン、ァセトニトリル、酢酸ェチルなど が例示でき、 1種単独または 2種以上混合して使用することもできる。  As the solvent used in the above reaction, a conventional solvent can be used, and examples thereof include water, methanol, ethanol, propanol, butanol, acetone, acetonitrile, and ethyl acetate, one kind alone or a mixture of two or more kinds. It can also be used.
上記反応は、通常— 10〜: L00°C程度、好ましくは 0〜36°C程度で行い、通常 5分 〜15時間程度で完了し、所望の式(1)のカルボスチリルイ匕合物を得ることができる。  The above reaction is usually carried out at about −10 to: about L00 ° C., preferably about 0 to 36 ° C., and is usually completed in about 5 minutes to 15 hours to obtain the desired carboschirily compound of formula (1). Obtainable.
[0025] 本発明において反応式 1における原料化合物(2)〜(5)は適当な塩であってもよく 、また適当な反応性誘導体であってもよい。 In the present invention, the raw material compounds (2) to (5) in Reaction Scheme 1 may be an appropriate salt or an appropriate reactive derivative.
本発明の式(1)で示されるカルボスチリルイ匕合物またはその塩は、立体異性体、光 学異性体及び溶媒和物(水和物、エタノレート等)を包含する。  The carbostyril compound or salt thereof represented by the formula (1) of the present invention includes stereoisomers, optical isomers and solvates (hydrates, ethanolates, etc.).
本発明の式(1)で示されるカルボスチリル化合物は、医薬的に許容される酸を作用 させることにより容易に酸付加塩とすることができ、本発明はこの酸付加塩をも包含す る。上記において、酸としては、例えば塩酸、硫酸、リン酸、臭化水素酸、ヨウ化水素 酸、硝酸等の無機酸、酢酸、シユウ酸、コハク酸、マレイン酸、フマル酸、リンゴ酸、酒 石酸、クェン酸、マロン酸、メタンスルホン酸、安息香酸、トリフルォロ酢酸、ベンゼン スルホン酸、ギ酸、トルエンスルホン酸等の有機酸、またはアミノ酸(たとえばアルギ- ン、ァスパラギン酸、グルタミン酸など)等を挙げることができる。  The carbostyril compound represented by the formula (1) of the present invention can be easily converted into an acid addition salt by the action of a pharmaceutically acceptable acid, and the present invention includes this acid addition salt. . In the above, examples of the acid include inorganic acids such as hydrochloric acid, sulfuric acid, phosphoric acid, hydrobromic acid, hydroiodic acid, and nitric acid, acetic acid, oxalic acid, succinic acid, maleic acid, fumaric acid, malic acid, and tartaric acid. Examples include acids, citrate, malonic acid, methanesulfonic acid, benzoic acid, trifluoroacetic acid, benzenesulfonic acid, formic acid, toluenesulfonic acid and other organic acids, or amino acids (eg, alginine, aspartic acid, glutamic acid, etc.) Can do.
[0026] また本発明の式(1)で示されるカルボスチリルイ匕合物は、医薬的に許容される塩基 性ィ匕合物を作用させることにより容易に塩を形成させることができる。それらの塩とし ては、例えば、アルカリ金属塩 (たとえばナトリウム塩、カリウム塩など)およびアルカリ 土類金属塩 (たとえばカルシウム塩、マグネシウム塩など)などの金属塩;アンモ-ゥ ム塩;有機塩基塩 (たとえばトリメチルァミン塩、トリェチルァミン塩、ピリジン塩、ピコリ ン塩、ジシクロへキシルァミン塩、 N、 N,—ジベンジルエチレンジァミン塩など)等を 挙げることができる。該塩基性化合物としては、例えば水酸ィ匕ナトリウム、水酸化カリ ゥム、水酸ィ匕カルシウム、炭酸ナトリウム、炭酸水素カリウム等を挙げることができる。 [0026] The carbostyril compound represented by the formula (1) of the present invention is a pharmaceutically acceptable base. A salt can be easily formed by allowing the chemical compound to act. Examples of such salts include metal salts such as alkali metal salts (for example, sodium salts and potassium salts) and alkaline earth metal salts (for example, calcium salts and magnesium salts); ammonium salts; organic base salts (For example, trimethylamine salt, triethylamine salt, pyridine salt, picolin salt, dicyclohexylamine salt, N, N, -dibenzylethylenediamine salt, etc.). Examples of the basic compound include sodium hydroxide, potassium hydroxide, calcium hydroxide, sodium carbonate, potassium hydrogen carbonate and the like.
[0027] また本発明の式(1)で示されるカルボスチリルイ匕合物は、通常の粉砕機 (例えばァ トマィザ一)によって粒子径を小さくすることにより、生体内への吸収をより効率よく行 うことができる。当該カルボスチリルイ匕合物の粒子径を微細化した粉末を製造する方 法は、当業者が良く知っている公知の方法により容易に粒子径を微細化することが できる。該方法は例えばミルの回転比、或いはカルボスチリルイ匕合物(1)の供給比な どの適当な条件下にセラミックミルによって微細化することができる。また本発明の式 (1)で示されるカルボスチリルイ匕合物の適当な供給比や回転比で回転させながら、 適当な供給空気圧でエア ジェットミルを通過させることによつても微細化することが できる。当該方法により製剤化に適した平均粒子径 0. 5〜5 ;ζ ΐη、 90%積算粒子径 10 μ m以下の本発明の式(1)で示されるカルボスチリルイ匕合物粉砕品を得ることが できる。 [0027] In addition, the carbostyril compound represented by the formula (1) of the present invention is more efficiently absorbed into the living body by reducing the particle diameter with a normal pulverizer (for example, an atomizer). It can be carried out. As a method for producing a powder having a reduced particle size of the carboschirirui compound, the particle size can be easily reduced by a known method well known to those skilled in the art. The method can be refined by a ceramic mill under suitable conditions such as the mill rotation ratio or the feed ratio of the carboschilli compound (1). It can also be refined by passing through an air jet mill with an appropriate supply air pressure while rotating at an appropriate supply ratio or rotation ratio of the carboschilli compound represented by the formula (1) of the present invention. Is possible. By this method, a pulverized product of carbostilil compound represented by the formula (1) of the present invention having an average particle size of 0.5 to 5; ζ ΐη and 90% cumulative particle size of 10 μm or less suitable for formulation is obtained. be able to.
実施例  Example
[0028] 以下に実施例を挙げて、本発明を更に詳細に説明する。  [0028] Hereinafter, the present invention will be described in more detail with reference to examples.
[0029] 実施例 1 [0029] Example 1
2 -ァセトアミド 2—エトキシカルボ-ル 3— [2 ( 1H) キノリノン 4 ィル]プ ロピオン酸ェチル(式(4)の化合物) 40gに、 20%塩酸 400ml、及びノルマルォクタ ノール 12mlをカ卩え、ディーン 'スターク装置を用いて、装置内で分離した凝縮液のう ちノルマルォクタノールを含む上層は反応缶に循環し、下層のみを 1時間当たり 10 〜20ml程度留去しながら 6時間還流した。還流 6時間後にノルマルォクタノールを留 去した後、更に 1時間当たり 10〜20ml程度留去しながら 2時間還流した。 20°C以下 に冷却後、析出した結晶を濾取した。得られた結晶をアセトンで洗浄し、約 60°Cで温 風乾燥して、 35. 4g (収率 97. 1%)の 2 ァミノ一 3— [2 (1H)—キノリノン一 4—ィ ル]プロピオン酸ニ塩酸塩二水和物(式(5)の化合物の二塩酸塩二水和物)を得た。 融点; 295°C (分解) 2-acetoamide 2-ethoxycarbol 3— [2 (1H) quinolinone 4-yl] ethyl ethion propionate (compound of formula (4)) 40 g, 20% hydrochloric acid 400 ml and normaloctanol 12 ml were added, Using the Dean 'Stark device, the upper layer containing normal octanol out of the condensate separated in the device was circulated to the reactor, and only the lower layer was refluxed for 6 hours while distilling about 10 to 20 ml per hour. . After 6 hours of reflux, the normal octanol was distilled off and then refluxed for 2 hours while distilling about 10 to 20 ml per hour. After cooling to below 20 ° C, the precipitated crystals were collected by filtration. The obtained crystals are washed with acetone and heated at about 60 ° C. After drying in air, 35.4 g (yield 97.1%) of 2-amino-1- (2 (1H) -quinolinone-4-yl] propionic acid dihydrochloride dihydrate (of formula (5) Compound dihydrochloride dihydrate) was obtained. Melting point: 295 ° C (decomposition)
1H-NMR (DMSO-d , δ ppm)  1H-NMR (DMSO-d, δ ppm)
6  6
11.81 (brs, IH), 8.67 (brs, 3H)、 7.85 (d, J=8.3 Hz, IH) , 7.54 (t, J=7.6Hz, IH), 7.3 8(d, J=8.3Hz, IH), 7.24 (t, J=7.6 Hz, IH), 6.51 (s, IH), 4.53—4.13 (m, IH), 3.37 (d, J=7.3 Hz, 2H)  11.81 (brs, IH), 8.67 (brs, 3H), 7.85 (d, J = 8.3 Hz, IH), 7.54 (t, J = 7.6Hz, IH), 7.3 8 (d, J = 8.3Hz, IH) , 7.24 (t, J = 7.6 Hz, IH), 6.51 (s, IH), 4.53—4.13 (m, IH), 3.37 (d, J = 7.3 Hz, 2H)
水分; 10.6% (理論値: 10.6%)  Moisture; 10.6% (theoretical value: 10.6%)
塩酸含量 ;21.0% (理論値 : 21.4%)  Hydrochloric acid content; 21.0% (theoretical value: 21.4%)
元素分析;測定値 C:41.98%, H:5.04%, N:8.07%  Elemental analysis; measured value C: 41.98%, H: 5.04%, N: 8.07%
計算値 C:42.24%, H:5.31%, N:8.21% (C H N CI O )  Calculated C: 42.24%, H: 5.31%, N: 8.21% (C H N CI O)
12 18 2 2 5  12 18 2 2 5
[0030] 実飾 12  [0030] Jewelery 12
式(4)のィ匕合物 80. Ogに水 360ml、濃塩酸 360ml、及びァセ卜フエノン 60mlをカロ え、ディーン 'スターク装置を用いて、装置内で分離した凝縮液のうちァセトフヱノンを 含む上層は反応缶に循環し、下層はその一部を留去しながら還流温度(103〜106 °C)で 10時間反応した。反応後、濃縮留去して、ァセトフエノンを回収した。 20°C以 下に冷却後、析出した結晶を濾取した。得られた結晶をアセトンで洗浄した後、約 60 °Cで温風乾燥して、二塩酸塩二水和物として所望の式(5)の化合物を得た (収率: 9 5. 6%)。  Compound of formula (4) 80. Add 360 ml of water, 360 ml of concentrated hydrochloric acid, and 60 ml of acetophenone to Og, and use acetophenone in the condensate separated in the apparatus using Dean's Stark device. The upper layer was circulated in the reaction vessel, and the lower layer was reacted for 10 hours at the reflux temperature (103 to 106 ° C.) while part of the lower layer was distilled off. After the reaction, the solution was concentrated and distilled to recover acetophenone. After cooling to below 20 ° C, the precipitated crystals were collected by filtration. The obtained crystals were washed with acetone and then dried in hot air at about 60 ° C. to obtain the desired compound of formula (5) as dihydrochloride dihydrate (yield: 95.6%) ).
[0031] 実施例 3 [0031] Example 3
2 -ァミノ 3— [2 ( 1H) キノリノン 4 ィル]プロピオン酸ニ塩酸塩二水和物( 式(5)の化合物の二塩酸塩二水和物) 30gに、水 600ml及び 25%の水酸化ナトリウ ム水溶液 60mlをカ卩えて溶解した。次に、 4 クロ口べンゾイルクロリド 23g (式(6)の 化合物)のアセトン 90ml溶液を氷冷下で滴下した。滴下終了後、塩酸酸性とし、析 出した結晶を濾取した。得られた結晶を水及びアセトンで洗浄し、約 80°Cで温風乾 燥して、 31. 6g (収率 96. 9%)の式(1)のカルボスチリルイ匕合物を得た。  2-Amino 3— [2 (1H) quinolinone 4-yl] propionic acid dihydrochloride dihydrate (dihydrochloride dihydrate of the compound of formula (5)) in 30 g, water 600 ml and 25% water 60 ml of an aqueous sodium oxide solution was added and dissolved. Next, a 90 ml acetone solution of 23 g (compound of formula (6)) of 4-clobenbenzoyl chloride was added dropwise under ice cooling. After completion of the dropwise addition, the solution was acidified with hydrochloric acid, and the precipitated crystals were collected by filtration. The obtained crystals were washed with water and acetone, and dried with warm air at about 80 ° C. to obtain 31.6 g (yield 96.9%) of a carbostyril compound of formula (1).
[0032] 実施例 4 [0032] Example 4
式(4)のィ匕合物 20gに水 90ml、濃塩酸 90ml、酢酸 60mlを加えて加熱し、 6時間 還流して反応させた。 125mlを濃縮留去し、 20°C以下に冷却後、析出した結晶を濾 取した。得られた結晶をアセトンで洗浄し、約 60°Cで温風乾燥して、式(5)の化合物 を得た (収率: 96. 2%) 0 Add 90 ml of water, 90 ml of concentrated hydrochloric acid and 60 ml of acetic acid to 20 g of the compound of formula (4) and heat for 6 hours. The reaction was carried out at reflux. 125 ml was concentrated and distilled off, and after cooling to 20 ° C. or lower, the precipitated crystals were collected by filtration. The obtained crystals were washed with acetone and dried with warm air at about 60 ° C, to give the compound of formula (5) (yield: 96.2%) 0
産業上の利用可能性  Industrial applicability
[0033] 本発明の方法によれば、高沸点溶剤の使用により突沸の危険を回避できるので、 所望の式(1)のカルボスチリルイ匕合物またはその塩を安全に製造することができ、ま た、反応缶の容積効率も格段に高めることができるので、大量合成に極めて有効で ある。 [0033] According to the method of the present invention, the danger of bumping can be avoided by using a high-boiling solvent, so that a desired carbostyril compound or salt thereof of the formula (1) can be produced safely, In addition, the volumetric efficiency of the reactor can be greatly increased, which is extremely effective for mass synthesis.
[0034] 本発明の方法によれば、使用した高沸点溶剤は、反応途中に留去した後、分液す るか、また反応終了後に留去液力も分液することにより容易に回収することができ、ま た、固液分離後の酸 (塩酸)濾液からは、単純な蒸留操作を行うことにより、初期の留 分を除いた大半の留分を廃棄することなく再使用可能な酸 (塩酸)として回収可能で あるため、環境に対する悪影響を軽減できる。  [0034] According to the method of the present invention, the high-boiling solvent used is easily recovered by distilling off during the reaction, or by separating the liquid after distilling off the reaction. In addition, the acid (hydrochloric acid) filtrate after solid-liquid separation can be reused without discarding the majority of the fractions except the initial fraction by performing a simple distillation operation. Since it can be recovered as (hydrochloric acid), adverse effects on the environment can be reduced.
[0035] 本発明の方法によれば、反応終了後の後処理は、冷却後に結晶濾取という簡単な 操作により、高収率で式(5)の化合物またはその塩を得ることができるので、式(1)の カルボスチリルイ匕合物またはその塩の大量合成に有効である。  [0035] According to the method of the present invention, the post-treatment after completion of the reaction can obtain the compound of formula (5) or a salt thereof in a high yield by a simple operation of crystal filtration after cooling. It is effective for the large-scale synthesis of the carboschiril compound of formula (1) or a salt thereof.
[0036] 本発明の式(5)の化合物の二塩酸塩二水和物は、他の公知の式(5)の化合物の 一塩酸塩と比べると濾過性が良ぐ遠心分離機等による結晶の取り出しが容易となる 。また、式(5)の化合物の二塩酸塩二水和物は、濾過性が良いことから含液率の低 V、湿体として得ることができるため、不純物が濾液側に除去され易くより高純度で得 ることができ、さらには乾燥が容易となることから、より効率的な大量製造を行うことが でき、目的化合物の中間体としてより保存に好適な新規物質である。  [0036] The dihydrochloride dihydrate of the compound of the formula (5) of the present invention is crystallized by a centrifuge or the like, which has better filterability than other known monohydrochlorides of the compound of the formula (5). It becomes easy to take out. In addition, since the dihydrochloride dihydrate of the compound of formula (5) has good filterability, it can be obtained as a low-liquid-content, low-humidity wet substance, so that impurities can be easily removed to the filtrate side. Since it can be obtained with a high degree of purity and can be easily dried, it can be mass-produced more efficiently and is a novel substance that is more suitable for storage as an intermediate of the target compound.
[0037] また本明細書に記載の方法によれば、式 (4)の化合物またはその塩から、式(5)の 化合物またはその塩に導く別の製造法として、式 (4)の化合物またはその塩を、一定 の使用割合の塩酸および酢酸の混合液中で加熱することで、高沸点溶剤を添加せ ずとも、発泡による界面上昇は、工業的な大量製造において許容できる程度まで抑 えられ、また比較的短時間に反応を完結させることもできる。  [0037] According to the method described in the present specification, as another production method leading from the compound of the formula (4) or a salt thereof to the compound of the formula (5) or a salt thereof, the compound of the formula (4) or By heating the salt in a mixture of hydrochloric acid and acetic acid at a certain ratio, the increase in the interface due to foaming can be suppressed to an acceptable level in industrial mass production without adding a high-boiling solvent. In addition, the reaction can be completed in a relatively short time.

Claims

請求の範囲 式 (4)の化合物またはその塩を、以下の(a)、または(a)および (b)の工程に付すこ とを特徴とする式(5)の化合物またはその塩の製造法: (a)酸性条件下、高沸点溶剤存在中、式 (4)の化合物またはその塩を加熱する工程 (b) (a)の工程において、反応副生物を留去する工程。 A process for producing a compound of the formula (5) or a salt thereof, characterized by subjecting the compound of the formula (4) or a salt thereof to the following steps (a) or (a) and (b): (A) A step of heating the compound of the formula (4) or a salt thereof in the presence of a high-boiling solvent under acidic conditions (b) A step of distilling off reaction by-products in the step (a).
[化 1] [Chemical 1]
Figure imgf000015_0001
Figure imgf000015_0001
[化 2]  [Chemical 2]
Figure imgf000015_0002
Figure imgf000015_0002
式 (4)の化合物またはその塩を、以下の(a)、または(a)および (b)の工程に付すこ とにより式(5)の化合物またはその塩を得る工程、さらに (c)の工程に付すことを特徴 とする式 (1)の化合物またはその塩の製造法:  A step of obtaining a compound of the formula (5) or a salt thereof by subjecting the compound of the formula (4) or a salt thereof to the following steps (a) or (a) and (b): A method for producing a compound of the formula (1) or a salt thereof characterized by being subjected to a process:
(a)酸性条件下、高沸点溶剤存在中、式 (4)の化合物またはその塩を加熱する工程  (a) A step of heating the compound of formula (4) or a salt thereof in the presence of a high boiling point solvent under acidic conditions
(b) (a)の工程において、反応副生物を留去する工程、 (b) a step of distilling off reaction by-products in the step (a);
(c)塩基性条件下、式(5)の化合物またはその塩を 4 クロ口べンゾイルク口リドと反 応させる工程。  (c) A step of reacting a compound of formula (5) or a salt thereof with 4-chlorobenzoyl chloride under basic conditions.
[化 3] NHCOCH3 [Chemical 3] NHCOCH3
' -COOEt  '-COOEt
で OOEt  In OOEt
(4)  (Four)
[化 4] [Chemical 4]
Figure imgf000016_0001
Figure imgf000016_0001
[化 5]  [Chemical 5]
Figure imgf000016_0002
Figure imgf000016_0002
(a)の工程が水中で行われ、および Zまたは、(c)の工程が水中もしくは有機溶媒 中またはその混合液中で行われることを特徴とする請求項 1または 2に記載の製造法  The process according to claim 1 or 2, wherein the step (a) is carried out in water, and the step Z or (c) is carried out in water, an organic solvent or a mixture thereof.
[4] (a)の工程における酸性条件が、塩酸酸性であることを特徴とする請求項 1から 3に 記載の製造法。 [4] The process according to any one of claims 1 to 3, wherein the acidic condition in the step (a) is hydrochloric acid acidity.
[5] 高沸点溶剤がノルマルォクタノールおよび Zまたはァセトフエノンであることを特徴 とする請求項 1から 4に記載の製造法。  [5] The production method according to any one of [1] to [4], wherein the high boiling point solvent is normaloctanol and Z or acetophenone.
[6] 式(5)示される化合物の二塩酸塩二水和物。 [6] Dihydrochloride dihydrate of the compound represented by formula (5).
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